CN102191383A - Treatment method for waste printed circuit board - Google Patents
Treatment method for waste printed circuit board Download PDFInfo
- Publication number
- CN102191383A CN102191383A CN2011101024103A CN201110102410A CN102191383A CN 102191383 A CN102191383 A CN 102191383A CN 2011101024103 A CN2011101024103 A CN 2011101024103A CN 201110102410 A CN201110102410 A CN 201110102410A CN 102191383 A CN102191383 A CN 102191383A
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- China
- Prior art keywords
- tin
- metal
- iron
- temperature
- filtrate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 44
- 239000002699 waste material Substances 0.000 title claims abstract description 28
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims abstract description 55
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 48
- 229910052751 metal Inorganic materials 0.000 claims abstract description 39
- 239000002184 metal Substances 0.000 claims abstract description 39
- 229910052755 nonmetal Inorganic materials 0.000 claims abstract description 28
- 229910052742 iron Inorganic materials 0.000 claims abstract description 23
- 239000000843 powder Substances 0.000 claims abstract description 21
- 238000000926 separation method Methods 0.000 claims abstract description 21
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 238000011084 recovery Methods 0.000 claims abstract description 8
- 238000007885 magnetic separation Methods 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims description 44
- 239000000706 filtrate Substances 0.000 claims description 30
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 24
- 229910017604 nitric acid Inorganic materials 0.000 claims description 24
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 23
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims description 13
- 239000012634 fragment Substances 0.000 claims description 13
- 238000001556 precipitation Methods 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 12
- MVFCKEFYUDZOCX-UHFFFAOYSA-N iron(2+);dinitrate Chemical compound [Fe+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MVFCKEFYUDZOCX-UHFFFAOYSA-N 0.000 claims description 12
- PIJPYDMVFNTHIP-UHFFFAOYSA-L lead sulfate Chemical compound [PbH4+2].[O-]S([O-])(=O)=O PIJPYDMVFNTHIP-UHFFFAOYSA-L 0.000 claims description 12
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 11
- 229910052763 palladium Inorganic materials 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 11
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 9
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 8
- 239000010949 copper Substances 0.000 claims description 8
- 229910052802 copper Inorganic materials 0.000 claims description 8
- 238000002386 leaching Methods 0.000 claims description 8
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 7
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 claims description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- -1 bronze ion Chemical class 0.000 claims description 6
- 229910052709 silver Inorganic materials 0.000 claims description 6
- 239000004332 silver Substances 0.000 claims description 6
- FAKFSJNVVCGEEI-UHFFFAOYSA-J tin(4+);disulfate Chemical compound [Sn+4].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O FAKFSJNVVCGEEI-UHFFFAOYSA-J 0.000 claims description 6
- 241000500881 Lepisma Species 0.000 claims description 5
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 5
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 5
- 229910052737 gold Inorganic materials 0.000 claims description 5
- 239000010931 gold Substances 0.000 claims description 5
- 239000000047 product Substances 0.000 claims description 5
- 229910000679 solder Inorganic materials 0.000 claims description 5
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 239000013078 crystal Substances 0.000 claims description 4
- 239000006148 magnetic separator Substances 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 229910052697 platinum Inorganic materials 0.000 claims description 4
- 230000001698 pyrogenic effect Effects 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- 239000004135 Bone phosphate Substances 0.000 claims description 3
- 229910000906 Bronze Inorganic materials 0.000 claims description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 3
- 239000004411 aluminium Substances 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052787 antimony Inorganic materials 0.000 claims description 3
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 claims description 3
- 239000010974 bronze Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 3
- 238000002425 crystallisation Methods 0.000 claims description 3
- 230000008025 crystallization Effects 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- 235000017550 sodium carbonate Nutrition 0.000 claims description 3
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 3
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 claims description 3
- 235000011152 sodium sulphate Nutrition 0.000 claims description 3
- 239000002023 wood Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 21
- 238000004070 electrodeposition Methods 0.000 description 9
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- RVPVRDXYQKGNMQ-UHFFFAOYSA-N lead(2+) Chemical compound [Pb+2] RVPVRDXYQKGNMQ-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 2
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 235000019253 formic acid Nutrition 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 description 1
- 229910017090 AlO 2 Inorganic materials 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 229910001369 Brass Inorganic materials 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 229910001128 Sn alloy Inorganic materials 0.000 description 1
- DPDMMXDBJGCCQC-UHFFFAOYSA-N [Na].[Cl] Chemical compound [Na].[Cl] DPDMMXDBJGCCQC-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- NICDRCVJGXLKSF-UHFFFAOYSA-N nitric acid;trihydrochloride Chemical compound Cl.Cl.Cl.O[N+]([O-])=O NICDRCVJGXLKSF-UHFFFAOYSA-N 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- XSNQEMWVLMRPFR-UHFFFAOYSA-N silver nitride Chemical compound [N-3].[Ag+].[Ag+].[Ag+] XSNQEMWVLMRPFR-UHFFFAOYSA-N 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 229910001432 tin ion Inorganic materials 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Processing Of Solid Wastes (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention provides a treatment method for a waste printed circuit board, which comprises the following steps of: wet sealing-off treatment, separation of lead and tin, rough crushing, magnetic separation of iron, vortex separation, fine crushing and separation of fine nonmetal powder, electrostatic separation of metal and nonmetal in coarse mixture, recovery of heat energy through fire burning and harmless treatment of harmful tail gas. The invention combines wet sealing-off, decomposing classification and fire burning to reasonably recover usable resources, and is environment-friendly.
Description
Technical field
The present invention relates to the processing of industrial waste, relate in particular to a kind of method of handling waste and old printed circuit board.
Background technology
The supporter that printed circuit board (PCB) is electrically connected as electronic devices and components in the electric equipment products is eliminated more and more along with the quickening of various electric equipment products update speed.These waste and old printed circuit boards are if directly abandoned, and with taking a large amount of land resourcess and causing the waste of valuable metal resource, wherein are no lack of rare precious metals such as gold and silver and palladium.In addition, it (mainly is the glass cloth that is compounded with the single or multiple lift of resins such as epoxy that printed circuit board base board is essentially macromolecular material, part is combined with metal pins and plastic pin), be difficult for degraded, multiple hazardous and noxious substances such as contained polyvinyl chloride and halogenide fire retardant will produce huge pollution to surrounding environment, also can produce objectionable constituent such as dioxin and lead steam if carry out burning disposal.Therefore, how effectively also waste and old printed circuit board is handled on environmental protection ground, realizes recycling, becomes problem demanding prompt solution.
Publication number is the novel process that 101569889 Chinese patent application discloses the high-valued clean utilization of a kind of waste printed circuit board total composition, wherein mainly adopt " disassembling classification-pyrogenic process-wet method combined flow process automatically " at first separating metal enrich body and non-metal powder, metal concentrate is sent into rotary incinerator and is burned, remove the resene organism, and with the recovery of separating low melting point such as slicker solder formation alloy, incineration tail gas discharges behind exhaust treatment system, will burn material and deliver to after the anode furnace redox refining metals such as recovering copper.But in this method metallic lead when liquid state and copper form alloy, high-temperature lower part divides volatilization to form obnoxious flavour, exist potential to pollute to environment, for avoiding occurring this environmental pollution, need in this method waste gas and dust access exhaust treatment system are focused on, this has just proposed higher requirement to system device, has increased the industrialization cost.In addition, only point out in this patent application that incineration tail gas discharges behind exhaust treatment system, but do not provide concrete solution.
Summary of the invention
For addressing the above problem, the present invention aims to provide a kind of method of handling waste and old printed circuit board, and employing wet method sealing-off-disassemble classification-pyrogenic process burning to combine is rationally recycled useful resources and environmentally friendly.
The invention provides a kind of method of handling waste and old printed circuit board, may further comprise the steps:
(1) the wet method sealing-off is handled: get waste and old printed circuit board, cleaning, drying, be immersed in and carry out the sealing-off processing in the nitric acid type tin stripping liquid, described waste and old printed circuit board must move back tinbase plate and components and parts after sealing-off is handled, move back tinbase plate and components and parts and enter step (3), its useless tin stripping liquid enters step (2);
(2) separate slicker solder: get useless tin stripping liquid described in the step (1), under 60～95 ℃ of temperature, begin to stir, add oxygenant, add alkali and go back to adjust pH to 2.5～3.0, reaction times 1～3h makes Fe
3+, Sn
4+Precipitation, and the lead bronze ion is stayed in the solution, the filtering separation solid-liquid gets stanniferous filter residue and leaded filtrate, reclaims tin and lead respectively;
(3) thick broken, magnetic separation separation of iron: will move back the tinbase plate described in the step (1) and components and parts utilize crusher in crushing to get fragment, fragment sorts out metallic iron through magnetic separator;
(4) eddy current sorting, the thin broken thin mouthful non-metal powder (VT powder) that separates: the fragment after the deironing grinds and the grading machine classification through vortex sorting machine, collect thin mouthful non-metal powder (VT powder) for thin mouthful from grading machine, collect for thick mouthful from grading machine and contain metal and nonmetallic thick mouthful of mixture;
(5) electrostatic separation separating metal and nonmetal: get and contain metal and nonmetallic thick mouthful of mixture, through electrostatic separator separating metal and nonmetal;
(6) pyrogenic process burns and reclaims heat energy: will burn in the nonmetal input incinerator of separating in the described step (5), reclaim heat energy, the tail gas of generation enters step (7);
(7) the harmful tail gas of harmless processing: tail gas is fed high-temperature incinerator, burn down, then gas is fed the rapid condensation system, temperature is cooled in 0.2s below 200 ℃ rapidly, at last gas is fed tank at 850～1200 ℃.
Wherein, step (1) splits waste and old printed circuit board for handling by sealing-off, and realization scolding tin removes fully and metallic lead and tin are carried out effective enrichment.
Usually, the tinsel layer that is plated on the circuit card and the copper between the base copper-layer-tin alloy thickness are 0.05 μ m～0.1 μ m, and As time goes on increase, so waste and old printed circuit board needs the scolding tin that removes that strong oxidizer could be strong.Tin stripping liquid of the present invention is the nitric acid type, and its oxidation system is made up of nitric acid and iron nitrate/iron(ic) chloride.Preferably, nitric acid type tin stripping liquid of the present invention comprises following component and weight percentage: nitric acid 15～50%, and iron nitrate or iron(ic) chloride 1～20%, sulfonic acid 1～5%, all the other are water.
Wherein, nitric acid is the main oxygenant of dissolving scolding tin, and can select mass percent for use is 68% nitric acid.Because tin is the torpescence metal, diluted acid and tin effect are very slow.Tin stripping liquid of the present invention is compared the concentration that existing tin stripping liquid has improved nitric acid, has effectively improved the erosion rate to scolding tin.
Fe in iron nitrate or the iron(ic) chloride
3+Have strong oxidizing property, add the oxidation capacity that iron nitrate or iron(ic) chloride can improve tin stripping liquid, and then effectively improve the speed of dissolving scolding tin, simultaneously, play the effect that promotes corrosion gunmetal layer.
In moving back the tin process, tin mainly is with Sn
2+Form exist in solution.Because Sn
2+Be oxidized to Sn by concentrated nitric acid, airborne oxygen etc. easily
4+, and Sn
4+Facile hydrolysis produces β-stannic acid precipitation, finally causes β-stannic acid attached to the dissolving that influences scolding tin on the scolding tin, so needs to add sulfonic acid in the tin stripping liquid.The effect of sulfonic acid be with solution in Sn
2+Form stable complex, promote the dissolving of scolding tin.Simultaneously, sulfonic acid is a kind of strong acid, can suppress the decomposition of nitric acid in the tin stripping liquid effectively.Consider that from raw materials cost more preferably, sulfonic acid is selected thionamic acid for use.
More preferably, tin stripping liquid of the present invention comprises following component and weight percentage: nitric acid 30～50%, and iron nitrate or iron(ic) chloride 10～18%, sulfonic acid 3～5%, all the other are water.Further preferably, tin stripping liquid of the present invention comprises following component and weight percentage: nitric acid 50%, and iron nitrate or iron(ic) chloride 18%, sulfonic acid 5%, all the other are water.
Because only being used for that the scolding tin on the waste and old printed circuit board is carried out sealing-off, handles tin stripping liquid of the present invention; and this class waste and old printed circuit board can not repeat to utilize again; need not to consider the protection to copper circuit on the circuit card, therefore tin stripping liquid of the present invention need not to add inhibiter.Tin stripping liquid component of the present invention is simple and to move back tin speed fast.
The preparation method of tin stripping liquid of the present invention comprises: get iron nitrate or iron(ic) chloride, sulfonic acid and be dissolved in fully in the water, add nitric acid, stir, make tin stripping liquid of the present invention.
In the step (1), preferably, the time that sealing-off is handled is 10～25min.Described waste and old printed circuit board enters step (3) after sealing-off is handled.
Tin metal content has great recovery value up to 60～100g/L (price of current tin metal up to 150,000 yuan/ton about) in the useless tin stripping liquid that forms in the sealing-off process.Simultaneously, it is that (the sealing-off process is only dissolved part metals lead for lead ion about 24～36g/L that useless tin stripping liquid also contains concentration, remaining undissolved metallic lead extracts in step (4)), in order to make lead and tin ion in the useless tin stripping liquid separately reclaim, the tin stripping liquid that will give up reclaims and enters step (2).
Step (2) is for separating slicker solder: get useless tin stripping liquid described in the step (1), under 60～95 ℃ of temperature, begin to stir, add oxygenant, add alkali and go back to adjust pH to 2.5～3.0, reaction times 1～3h makes Sn
4+Precipitation, and lead ion is stayed in the solution, the filtering separation solid-liquid gets stanniferous filter residue and leaded filtrate, reclaims tin and lead respectively.Wherein, oxygenant can be common oxygenants such as hydrogen peroxide or sodium chlorate.
Consider in the stanniferous filter residue to mix the iron ion that has concentration lower, and may mix the cupric ion that has concentration lower in the leaded filtrate, preferably, stanniferous filter residue and/or leaded filtrate further can be purified.
Preferably, step (2) reclaims tin for purifying the stanniferous filter residue: get the pulp of stanniferous filter residue water, add S-WAT and be reduced into Sn (OH)
2Precipitation adds alkali again and regulates pH value to 13～14, reacts 1～4h under 50～95 ℃ of temperature, makes Sn (OH)
2Precipitation becomes the [Sn (OH) of solubility
4]
2-, filtering, filter residue is an ironic hydroxide, returns leaching, filtrate adds sulfuric acid, goes back to adjust pH to 3～7, feasible [Sn (OH)
4]
2-Become Sn (OH)
2, filter, Sn (OH)
2Go back to adjust pH to 0.5～1 with acid, be dissolved into tin sulphate solution, the reconcentration crystallization becomes the tin sulphate crystal.
Preferably, step (2) reclaims the plumbous purifying lead-bearing filtrate that is: get leaded filtrate, add sodium sulfate according to plumbous excess coefficient 1.1～1.5 under 60～95 ℃ of temperature of temperature, stir reaction down 0.5～5 hour, filter, filter residue is a lead sulfate, and filtrate is cupric filtrate; After getting the pulp of filter residue lead sulfate, add yellow soda ash under 60～95 ℃ of temperature, regulate pH value to 9～10, reaction 2～5h makes lead sulfate change into the lead sulfate tribasic product.Cupric filtrate can change the solution after the leaching of step (5) over to.Preferably, cupric filtrate can be used for further preparing brass work.
Step (3)～(5) are for disassembling assorting process.
Step (3) comprises thick broken and magnetic separation separation of iron.To move back the tinbase plate described in the step (1) and components and parts utilize crusher in crushing to get fragment, fragment sorts out metallic iron through magnetic separator, and sorting index reaches more than 99%.
Step (4) comprises eddy current sorting, the thin broken thin mouthful non-metal powder (VT powder) that separates.Fragment after the deironing grinds and the grading machine classification through vortex sorting machine.The eddy current sorting is with an eddy current mill fragment after the deironing to be milled to below the 1mm.Grading machine has two outlets, and one is thick mouthful, one is thin mouthful, and what carefully come out in the mouth is thin mouthful non-metal powder (VT powder), and what come out in the thick mouth is metal and nonmetallic mixture.The major ingredient of thin mouthful of non-metal powder (VT powder) is glass fibre and thermosetting resin, can be used as the raw material of making plastic-wood section, and preferably, thin mouthful of non-metal powder (VT powder) further enters in the flow process of preparation plastic-wood section.Also preferably, thin mouthful of non-metal powder (VT powder) further is admitted to and burns recovery heat energy in the incinerator.
Step (5) is an electrostatic separation separating metal and nonmetal.Get from thick mouthful collect contain metal and nonmetallic thick mouthful of mixture drops into electrostatic separator, realize that by metallic conduction, nonmetal nonconducting principle metal separates with nonmetallic.Electrostatic separation operation end has three outlets, and that one of them outlet sub-elects is nonmetal, outlet sub-elects metal and non-metal mixture (internal recycle), another outlet sub-elect metal.Wherein, metal and non-metal mixture can reenter in the vortex sorting machine in the step (4) and carry out sorting, and so circulation realized metal and nonmetallic thorough the separation.
Preferably, separate in the step (5) metal be used for further extracting valuable metal, realize the maximization of valuable metal resource regeneration.More preferably, described valuable metal is selected from one or more in metallic lead, antimony, aluminium, copper, nickel, silver, gold, platinum and the palladium.
Step (6) reclaims heat energy for pyrogenic process burns.To burn in the nonmetal input incinerator of separating in the described step (5), wherein the combustion heat of plastics is very high, and the waste plastic combustionvelocity is fast, and ash content is low, adopts burning disposal energy efficient recovery heat energy.The tail gas that burns the back generation contains dioxin, and the high-temperature incinerator that feeds in the step (7) carries out pyroprocessing.
Step (7) is the harmful tail gas of harmless processing.Tail gas is fed high-temperature incinerator, burn down at 850～1200 ℃.Contain dioxin ， dioxin in the described tail gas and after burning, be decomposed into gas (CO
2, HCl and H
2O).Then these gases are fed the rapid condensation system, temperature is cooled to below 200 ℃ in 0.2s rapidly.At last these gases are fed tank.The reason of quick cooling is because after dioxin at high temperature decomposes, if cooling slowly, can regenerate in 300～500 ℃ interval, the temperature province that regenerates that therefore adopts the method for quick cooling directly to cross dioxin, He Cheng dioxin once more not in the quick cooling process.Cooling system can be spray cooler.
A kind of method of handling waste and old printed circuit board provided by the invention has following beneficial effect: employing wet method sealing-off-disassemble classification-pyrogenic process burning to combine, rationally reclaim valuable metal such as metallic lead and tin and reclaim useful resources such as heat energy, can realize the maximization of resource regeneration, environmental friendliness, simultaneously can solve waste and old printed circuit board and arbitrarily abandon the problem that causes taking a large amount of land resourcess, and can solve in the waste and old printed circuit board poisonous and harmful material the pollution problem of environment.
Embodiment
The following stated is a preferred implementation of the present invention; should be pointed out that for those skilled in the art, under the prerequisite that does not break away from the principle of the invention; can also make some improvements and modifications, these improvements and modifications also are considered as protection scope of the present invention.
Embodiment one
Exempt to burn the method that waste and old printed circuit board is handled in no cyaniding, may further comprise the steps:
(1) sealing-off is handled:
Get iron nitrate or iron(ic) chloride, sulfonic acid and be dissolved in fully in the water, add nitric acid, stir, make nitric acid type tin stripping liquid of the present invention according to following proportioning: nitric acid 40%, iron nitrate or iron(ic) chloride 16%, sulfonic acid 4%, all the other are water;
Get waste and old printed circuit board, cleaning, drying are immersed in and carry out the sealing-off processing in the nitric acid type tin stripping liquid, and described waste and old printed circuit board enters step (3) after sealing-off is handled 10min, and useless tin stripping liquid enters step (2).
(2) separate slicker solder:
Get described in the step (1) useless tin stripping liquid, record and wherein contain tin metal 60g/L, lead ion 22g/L, iron ion 19g/L and cupric ion 10g/L;
Under 60 ℃ of temperature, begin to stir, add oxidant hydrogen peroxide, add alkali and return adjust pH to 2.7, reaction times 3h makes Fe
3+, Sn
4+Precipitation, and the lead bronze ion is stayed in the solution, the filtering separation solid-liquid gets stanniferous filter residue and leaded filtrate.
Purify the stanniferous filter residue: get the pulp of stanniferous filter residue water, add S-WAT and be reduced into Sn (OH)
2Precipitation adds alkali again and regulates pH value to 13, reacts 3h under 60 ℃ of temperature, makes Sn (OH)
2Precipitation becomes the [Sn (OH) of solubility
4]
2-, filtering, filter residue is an ironic hydroxide, returns leaching, filtrate adds sulfuric acid, returns adjust pH to 3, feasible [Sn (OH)
4]
2-Become Sn (OH)
2, filter, Sn (OH)
2Return adjust pH to 0.5 with acid, be dissolved into tin sulphate solution, the reconcentration crystallization becomes the tin sulphate crystal.
Purifying lead-bearing filtrate: get leaded filtrate, add sodium sulfate according to plumbous excess coefficient 1.2 under 60 ℃ of temperature of temperature, stir reaction down 4 hours, filter, filter residue is a lead sulfate, and filtrate is cupric filtrate; After getting the pulp of filter residue lead sulfate, add yellow soda ash under 80 ℃ of temperature, regulate pH value to 9, reaction 4h makes lead sulfate change into the lead sulfate tribasic product.Cupric filtrate changes the solution after the leaching of step (5) over to.
(3) thick broken, magnetic separation separation of iron: will move back the tinbase plate described in the step (1) and components and parts utilize crusher in crushing to get fragment, fragment sorts out metallic iron through magnetic separator, and sorting index reaches 99.5%.
(4) eddy current sorting, the thin broken VT powder that separates: the fragment after the deironing grinds and the grading machine classification through vortex sorting machine, collects the VT powder for thin mouthful from grading machine, collects for thick mouthful from grading machine and contains metal and nonmetallic thick mouthful of mixture.
(5) electrostatic separation separating metal and nonmetal: get the thick mouthful of mixture of collecting from thick mouthful, through electrostatic separator separating metal and nonmetal.
Isolated metal and NaOH: NaNO
3=1: 1 fusing agent mixes by 1: 1 mass ratio, at 550 ℃ of following low smelting heat 1h, filters, and filtrate obtains Na after evaporation concentration
2SbO
3And Na
2AlO
2Mixed crystal, mother liquid evaporation return the water logging operation.Get the filter residue that removes antimony and aluminium, add 3.5mol/L sulphuric acid soln and hydrogen peroxide, under 70 ℃ of temperature, leach 2h, the solution after leaching is filtered, eddy flow selectivity electro deposited copper, its electrodeposition condition is: electrolyte ph is 5.0, and temperature is 60 ℃, and current density is 550A/m
2, the electrodeposition time is 0.5h, obtains electro deposited copper.The long-pending back of power taking liquid eddy flow selectivity electro deposited nickel, its electrodeposition condition is: electrolyte ph is 5.0, and temperature is 70 ℃, and current density is 450A/m
2, the electrodeposition time is 0.5h, obtains electro deposited nickel, liquid returns the sulfuric acid leaching behind the electrodeposition.Get the copper removal filter residue, by the concentration with salpeter solution is that 1: 1 adding salpeter solution dissolves silver and palladium, the control extraction temperature is 85 ℃ of leaching 0.5h, the filtering separation solid-liquid, the filter residue of the filtrate of argentiferous, palladium and desilver, palladium, control pH value is 5 in the filtrate of argentiferous, palladium subsequently, and normal temperature constantly stirs down, adds NaOH solution, make the palladium precipitation, silver ions is stayed in the solution, and the filtering separation solid-liquid gets argentiferous filtrate and contains the palladium throw out, add sodium-chlor to described argentiferous filtrate, make the silver precipitation, the filtering separation solid-liquid gets silver nitride precipitation.Get desilver, palladium filter residue, add the chloroazotic acid of 5 times of quality, the speed with 1000r/min under 70 ℃ of temperature stirs, and leaches 1h; Leach liquor eddy flow electrodeposition gold, its electrodeposition condition is: temperature is 60 ℃, current density is 400A/m
2, the electrodeposition time is 0.5h, electrolyte ph is 5.5, obtains the electrodeposition gold.The long-pending back of power taking liquid adds saturated NH
4Cl reaction 8h after-filtration, filter residue is an ammonium chloroplatinate, obtains spongy platinum after refining.Get and remove platinum filtrate, by palladium: the formic acid mass ratio is 3: 1 a ratio adding formic acid, reacts 0.5h under 90 ℃ of intensively stirred conditions, and the pH value is controlled at 9.0, obtains thick palladium powder.
(6) pyrogenic process burns and reclaims heat energy: will burn in the nonmetal input incinerator of separating in the described step (5), reclaim heat energy, the tail gas of generation enters step (7).
(7) the harmful tail gas of harmless processing: tail gas is fed high-temperature incinerator, burn down at 1000 ℃, the De dioxin is decomposed into gas CO in the tail gas
2, HCl and H
2O feeds the rapid condensation system with these gases then, and temperature is cooled to 180 ℃ rapidly in 0.1s, at last the gas after the quick cooling is fed tank.
The method employing wet method sealing-off of processing waste and old printed circuit board provided by the invention-disassemble classification-pyrogenic process burning to combine, rationally reclaim valuable metal such as metallic lead and tin and reclaim useful resources such as heat energy, can realize the maximization of resource regeneration, environmental friendliness.
Claims (10)
1. a method of handling waste and old printed circuit board is characterized in that, may further comprise the steps:
(1) the wet method sealing-off is handled: get waste and old printed circuit board, cleaning, drying, be immersed in and carry out the sealing-off processing in the nitric acid type tin stripping liquid, described waste and old printed circuit board must move back tinbase plate and components and parts after sealing-off is handled, move back tinbase plate and components and parts and enter step (3), its useless tin stripping liquid enters step (2);
(2) separate slicker solder: get useless tin stripping liquid described in the step (1), under 60～95 ℃ of temperature, begin to stir, add oxygenant, add alkali and go back to adjust pH to 2.5～3.0, reaction times 1～3h makes Fe
3+, Sn
4+Precipitation, and the lead bronze ion is stayed in the solution, the filtering separation solid-liquid gets stanniferous filter residue and leaded filtrate, reclaims tin and lead respectively;
(3) thick broken, magnetic separation separation of iron: will move back the tinbase plate described in the step (1) and components and parts utilize crusher in crushing to get fragment, fragment sorts out metallic iron through magnetic separator;
(4) eddy current sorting, the thin broken thin mouthful non-metal powder that separates: the fragment after the deironing grinds and the grading machine classification through vortex sorting machine, collects thin mouthful non-metal powder for thin mouthful from grading machine, collects for thick mouthful from grading machine and contains metal and nonmetallic thick mouthful of mixture;
(5) electrostatic separation separating metal and nonmetal: get described thick mouthful of mixture, through electrostatic separator separating metal and nonmetal;
(6) pyrogenic process burns and reclaims heat energy: will burn in the nonmetal input incinerator of separating in the described step (5), reclaim heat energy, the tail gas of generation enters step (7);
(7) the harmful tail gas of harmless processing: tail gas is fed high-temperature incinerator, burn down, then gas is fed the rapid condensation system, temperature is cooled in 0.2s below 200 ℃ rapidly, at last gas is fed tank at 850～1200 ℃.
2. the method for claim 1 is characterized in that, nitric acid type tin stripping liquid comprises following component and weight percentage described in the step (1): nitric acid 15～50%, and iron nitrate or iron(ic) chloride 1～20%, sulfonic acid 1～5%, all the other are water.
3. method as claimed in claim 2 is characterized in that, described nitric acid type tin stripping liquid comprises following component and weight percentage: nitric acid 30～50%, and iron nitrate or iron(ic) chloride 10～18%, sulfonic acid 3～5%, all the other are water.
4. method as claimed in claim 3 is characterized in that, described nitric acid type tin stripping liquid comprises following component and weight percentage: nitric acid 50%, and iron nitrate or iron(ic) chloride 18%, sulfonic acid 5%, all the other are water.
5. the method for claim 1 is characterized in that, the time that described sealing-off is handled is 10～25min.
6. the method for claim 1 is characterized in that, the described recovery tin of step (2) is for purifying the stanniferous filter residue: get the pulp of stanniferous filter residue water, add S-WAT and be reduced into Sn (OH)
2Precipitation adds alkali again and regulates pH value to 13～14, reacts 1～4h under 50～95 ℃ of temperature, makes Sn (OH)
2Precipitation becomes the [Sn (OH) of solubility
4]
2-, filtering, filter residue is an ironic hydroxide, returns leaching, filtrate adds sulfuric acid, goes back to adjust pH to 3～7, feasible [Sn (OH)
4]
2-Become Sn (OH)
2, filter, Sn (OH)
2Go back to adjust pH to 0.5～1 with acid, be dissolved into tin sulphate solution, the reconcentration crystallization becomes the tin sulphate crystal.
7. the method for claim 1, it is characterized in that, the described recovery of step (2) is plumbous to be purifying lead-bearing filtrate: get leaded filtrate, under 60～95 ℃ of temperature of temperature, add sodium sulfate according to plumbous excess coefficient 1.1～1.5, stir reaction down 0.5～5 hour, filter, filter residue is a lead sulfate, and filtrate is cupric filtrate; After getting the pulp of filter residue lead sulfate, add yellow soda ash under 60～95 ℃ of temperature, regulate pH value to 9～10, reaction 2～5h makes lead sulfate change into the lead sulfate tribasic product.
8. the method for claim 1 is characterized in that, the thin mouthful of non-metal powder of collecting in the described step (4) is further used for preparing plastic-wood section or is admitted to and burn recovery heat energy in the incinerator.
9. the method for claim 1 is characterized in that, the metal of separating in the described step (5) is used for further extracting valuable metal, and valuable metal is selected from one or more in metallic lead, antimony, aluminium, copper, nickel, silver, gold, platinum and the palladium.
10. the method for claim 1 is characterized in that, contain dioxin ， dioxin described in the described step (7) in the tail gas and after burning, decompose, and in the quick cooling process He Cheng dioxin once more not.
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|---|---|---|---|
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Effective date of registration: 20201208 Address after: 331100 Jiangxi Yichun Fengcheng city resources recycling industry base Patentee after: JIANGXI GREEN ECO-MANUFACTURE RESOURCE CYCLE Co.,Ltd. Address before: Xinghua Road on the south side of the 518000 Guangdong city of Shenzhen province Baoan District Baoan District Center Rongchao Binhai building A building 20 room 2008 Patentee before: Grammy Corp. |
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Address after: 331100 Jiangxi Yichun Fengcheng city resources recycling industry base Patentee after: Jiangxi Green Recycling Industry Co.,Ltd. Address before: 331100 Jiangxi Yichun Fengcheng city resources recycling industry base Patentee before: JIANGXI GREEN ECO-MANUFACTURE RESOURCE CYCLE Co.,Ltd. |
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